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International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 1 Hydrogen Safety Training for Researchers and Technical Personnel Salvador Aceves,

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Presentation on theme: "International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 1 Hydrogen Safety Training for Researchers and Technical Personnel Salvador Aceves,"— Presentation transcript:

1 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 1 Hydrogen Safety Training for Researchers and Technical Personnel Salvador Aceves, Francisco Espinosa, Guillaume Petitpas, Tim Ross, Vernon Switzer International Conference on Hydrogen Safety San Francisco, CA September 12, 2011

2 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 2  Laboratory researchers handling small amounts of hydrogen  Technical personnel in charge of assembling and testing systems Appropriate H 2 safety instruction is key to avoiding accidents

3 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 3  Web-based class (4 hours) teaches basic information on pressure, cryogenics, flammability, asphyxiation, and other risks and precautions for using hydrogen  Hands-on safety class (3 days) teaches detailed component information as well as design, assembly, and testing of H 2 systems We are developing training materials targeting these two key groups

4 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 4 We have produced and peer reviewed a web-based hydrogen safety class for researchers  Four hours long  Six modules:  Introduction  Hydrogen properties  Pressure safety  Cryogenic safety  Emergency response  Codes and standards  End of module quizzes (passing grade 85%)  Web address:

5 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 5 Class demonstration: pressure safety module

6 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 6 3-day hands-on safety class First day: Classroom discussion on detailed component characteristics 1.Definitions 2.Hazards 3.Personal Protective Equipment (PPE) 4.Gas Cylinders 5.Gas Cylinder Manifold 6.Pressure Reducing Regulators 7.Gauges/Pressure Transducers 8.Regulator Safety Manifold 9.Relief Devices 10.Valves 11.Fittings 12.Tubing and Piping 13.Flash Arrestors 14.Quiz

7 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 7 First day of hands-on class: Classroom discussion on detailed component characteristics 1.Definitions 2.Hazards 3.Personal Protective Equipment (PPE) 4.Gas Cylinders 5.Gas Cylinder Manifold 6.Pressure Reducing Regulators 7.Gauges/Pressure Transducers 8.Regulator Safety Manifold 9.Relief Devices 10.Valves 11.Fittings 12.Tubing and Piping 13.Flash Arrestors 14.Quiz Example: class materials for pressure reducing regulators

8 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 8 Pressure Reducing Regulators Regulator Types –Single stage –Two-stage –Back pressure –Dome loaded

9 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 9 Pressure Reducing Regulators Single Stage Regulator Two Typical Applications: High Pressure –Manifold Regulator –High Flows Low Pressure –Line Station Regulator –Low Flows

10 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 10 Pressure Reducing Regulators

11 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 11 Pressure Reducing Regulators Two Stage Regulator Applications: –Precise Control –Lower Pressures –Lower Flows –Minimal Supply Pressure Effect

12 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 12 Pressure Reducing Regulators Back Pressure Regulator Applications: –Controlling Pump Pressures –Fluid Sampling –Industrial Controls –Adjustable Relief for Test Consoles

13 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 13 Pressure Reducing Regulators Dome Loaded Regulator Applications: –High Pressure –High Flow Purge –Manifold Regulator –Test Consoles

14 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 14 Pressure Reducing Regulators

15 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 15 Pressure Reducing Regulators Cylinder Relief Devices –Type: Spring loaded Frangible disc Fusible plug Frangible disk backed by fusible metal No relief device –Use: propane, mapp gas CO 2, N 2, O 2, argon, He acetylene, chlorine hydrogen, methane arsine, fluorine, phosgene

16 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 16 Pressure Reducing Regulators Compressed Gas Cylinder Handling –DOT cylinder identification –*,+, Hydro test date –Cylinder status tag –Use proper discharge controls –Keep cylinders away from heat

17 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 17 Pressure Reducing Regulators Always –Read the shoulder label on the cylinder, verify gas –Select the proper regulator for the gas being used –Secure the cylinder before installing the regulator –Inspect the cylinder valve and regulator for damage

18 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 18 Pressure Reducing Regulators Always (continued) –Make sure the cylinder valve and regulator connections are free of dirt, oil, grease, and foreign material –Close the regulator by turning the pressure control knob counterclockwise until the knob turns freely without tension before opening the cylinder valve –Open the cylinder valve slowly

19 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 19 Pressure Reducing Regulators Never –Use a damaged regulator –Adjust, remove, or plug relief devices –Change CGA or inlet connection –Lubricate any part of the regulator or cylinder valve

20 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 20 Pressure Reducing Regulators Never (continued) –Force threaded connections –Stand in front of the regulator while opening the cylinder valve –Attempt to perform any type of repair to the regulators, consult an authorized repair shop

21 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 21 Glossary –Droop This is the amount of outlet pressure decrease with respect to increasing flow demand on a pressure reducing regulator. It can be expressed in percentage change of the set point or can be shown as pounds per square inch change with respect to flow increases –Lockup This is the amount of outlet pressure increase beyond the set pressure with respect to decreasing flow demand on a pressure reducing regulator. –Critical Flow This is also sometimes referred to as sonic flow and is the maximum flow which can pass through a regulator or an orifice Pressure Reducing Regulators

22 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 22 Pressure Reducing Regulators Glossary (continued) –Creep This is an increase in outlet pressure occurring after lockup. Creep normally appears as a gradual rise in outlet pressure over a period of time. The usual cause of creep is contamination in the regulator seat causing the regulator to remain slightly open henceforth additional outlet pressure. –Bubble Tight Shutoff Determined by connecting the outlet of a regulator with a piece of tubing and submerging the end under an inch or two of water. With inlet pressure applied and the regulator in an off condition, there should not be any bubbles within a time period of one minute. This constitutes “Bubble Tight Shutoff”. –Set Point This is the control point desired for operation of a regulator.

23 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 23 Pressure Reducing Regulators Glossary (continued) –CGA Fittings Compressed Gas Association (CGA) is the group that has established standards in the gas industry for fittings which are used to attach to gas cylinders. –DIN Fittings Deutsches Institut für Normung (DIN), English translation would be German Industrial Standard. The DIN system was developed by Germans and is used in Europe. –Coefficient of flow (C v ) For a valve is the volume of water in U.S. gallons per minute at room temperature…which will flow through the valve with the stem fully open…with a pressure drop of 1 psi across the valve. C v is the valve sizing factor that permits selection of the appropriate valve to meet the flow requirements of a given fluid system.

24 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 24 Relief device pressure gauge CGA fitting We have developed a variety of instructional materials for 3-day hands-on hydrogen safety class Working table pressure vessels regulator

25 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 25 Second day: assemble pressure system described in engineering safety note

26 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 26 Second day: assemble pressure system described in engineering safety note

27 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 27 Second day: video illustrates planning, component installation, tube cutting and bending, compression fittings, and leak testing using mass spectrometer leak detector

28 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 28 Third day: video illustrates data acquisition setup, pressure test, leak test at MOP, and system operation

29 International Conference on Hydrogen Safety, LLNL, September 12, 2011, p. 29 Summary  We are contributing to safe hydrogen operations by developing instructional materials for researchers and operators  Web-based class (now complete) addresses the need of laboratory researchers handling small amounts of hydrogen  Hands-on class (in process) will present in-depth information for technical personnel tasked with installing and testing hydrogen systems  Participation from the hydrogen community will improve the class through suggestions, bug reports, etc.


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